Integrative reductant system and method using constant volume injection

ABSTRACT

Various embodiments relate to a selective catalytic reduction system for treating exhaust gases of an internal combustion engine. The system includes an inlet section that receives exhaust gases from the engine. The system includes a tank storing diesel exhaust fluid (“DEF”), a pump, a valve, and an injector each in fluid communication with each other. The injector is coupled to the inlet exhaust pipe and configured to inject DEF into the exhaust gases flowing through the inlet exhaust pipe in a plurality of pulses. Each of the plurality of pulses injects a constant volume of DEF into the inlet exhaust pipe. The system further includes a controller configured to operate the pump and the valve such that a time interval between successive constant volume pulses of the plurality of pulses is varied based on a variable oxides of nitrogen content of the exhaust gases.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No.14/859,755, filed on Sep. 21, 2015, which claims the benefit of andpriority to U.S. Provisional Patent Application No. 62/055,963, filed onSep. 26, 2014, which are herein incorporated by reference in theirentirety.

TECHNICAL FIELD

The present disclosure relates generally to exhaust aftertreatmentsystems for internal combustion engines.

BACKGROUND

Internal combustion engines generate exhaust gases during combustion.The exhaust gases often contain contaminants that, when left untreated,can harm the environment. The contaminants include oxides of nitrogen(“NOx”), which can react with atmospheric air to form smog, ozone, andacid rain. Although there are many different oxides of nitrogen (e.g.,nitrogen monoxide, nitrogen dioxide, nitrous oxide, nitroslyazide,nitrate radical, etc.) used herein, NOx primarily refers to nitrogenmonoxide and nitrogen dioxide. Oxides of nitrogen other than nitrogenmonoxide and nitrogen dioxide are not generally regulated by internalcombustion engine emissions standards. Many regulatory territories(e.g., the United States, the European Union, India, China, etc.)regulate the amount of NOx that is permitted to vent into the ambientenvironment from internal combustion engines. Accordingly, exhaustaftertreatment systems are employed. For example, some internalcombustion engines utilize a selective catalytic reduction (“SCR”)system that injects diesel exhaust fluid (“DEF”) into the exhauststream. The DEF is a liquid that typically includes urea. When the ureais heated by the exhaust gases, the urea breaks down into ammonia, whichreacts with NOx to form water and nitrogen thereby reducing NOxemissions.

Many SCR systems inject a variable dose of DEF into the exhaust stream(e.g., into an exhaust component carrying exhaust gases from theinternal combustion engine) at constant time intervals. In such systems,the amount of DEF dosed into the exhaust stream is varied depending onthe amount of NOx in the exhaust stream. For example, at engine idlespeeds, a first amount of DEF may be dosed into the exhaust stream at agiven time interval, and during higher than idle engine operatingspeeds, a second amount of DEF, which is larger than the first amount,may be dosed into the exhaust stream at the same given time interval.The fixed interval between successive doses may occur every millisecond.

However, such fixed interval, variable amount SCR systems have numerousdrawbacks. Variable volume injectors can suffer from inaccurate doses ofDEF (e.g., 20-30% error in the amount of DEF actually dosed vs. theamount of DEF intended to be dosed)—particularly at low volume doses ofDEF. Further, under certain conditions, particularly at lower thannormal exhaust gas temperatures (e.g., less than 200 degrees Celsius),excess DEF can form deposits or film on the various exhaust gascomponents. In some situations, deposits or film can form under normaloperating conditions at locations where continual dosing can lower localtemperatures on impingement surfaces even though there is adequate heatin the exhaust stream to decompose the DEF. Fixed interval, variableamount SCR systems can also require sophisticated controllers, high costDEF pumps, and more complicated and less robust injectors.

Further, fixed interval, variable amount SCR systems often utilize asingle reductant injector. The single injector continuously sprays thereductant into a component of the aftertreatment system, where thereductant is at least partially broken down into ammonia by the heat ofthe exhaust gases and the heat of the component of the aftertreatmentsystem. However, the continuous spraying of the reductant into thecomponent may result in localized cold spots on the wall of thecomponent where the reductant contacts the component. The localized coldspots may inhibit the breakdown of the reductant into ammonia.Accordingly, reductant deposits and films can form in the areas of thecold spots of the component. Such deposits and films may be mitigatedthrough heating of the component with a secondary heating device orthrough modulation of the quantity of reductant injected. However, thesesolutions require auxiliary emission control devices that can drive upthe cost and complexity of the aftertreatment system.

SUMMARY

One example embodiment relates to an aftertreatment system for treatingexhaust gases of an internal combustion engine. The system includes aninlet exhaust pipe configured to receive the exhaust gases from theinternal combustion engine. The system includes a tank storing areductant, such as DEF, a pump in fluid communication with the tank, avalve in fluid communication with the pump, and an injector in fluidcommunication with the valve. The injector is coupled to the inletexhaust pipe and configured to inject the reductant into the exhaustgases flowing through the inlet exhaust pipe in a plurality of pulses.Each of the plurality of pulses injects a constant volume of reductantinto the inlet exhaust pipe. The system further includes a controllerconfigured to operate the pump and the valve such that a time intervalbetween successive constant volume pulses of the plurality of pulses isvaried based on a variable oxides of nitrogen content of the exhaustgases.

Another example embodiment relates to an aftertreatment system fortreating exhaust gases of an internal combustion engine. The systemincludes an inlet exhaust pipe configured to receive the exhaust gasesfrom the internal combustion engine. The system further includes a valvein fluid communication with a reductant source that provides a liquidreductant to the valve. The system includes an injection device in fluidcommunication with the valve. The injection device is coupled to theinlet exhaust pipe and is configured to inject the liquid reductant intothe exhaust gases flowing through the inlet exhaust pipe in a pluralityof pulses. Each of the plurality of pulses injects a constant volume ofthe liquid reductant into the inlet exhaust pipe. The system furtherincludes a controller configured to operate the pump and the valve suchthat a time interval between successive constant volume pulses of theplurality of pulses is varied based on a variable oxides of nitrogencontent of the exhaust gases.

A further example embodiment relates to a method. The method includesreceiving, by a controller of an exhaust aftertreatment system for aninternal combustion engine, feedback from an exhaust sensor of theexhaust aftertreatment system. The method further includes determining,by the controller, an amount of a liquid reductant to be injected intoan inlet section of the exhaust after treatment system based at least inpart on the feedback from the exhaust sensor. The method includesdetermining, by the controller, that the amount of the liquid reductantto be injected is equal to a threshold amount of liquid reductant. Thethreshold amount of liquid reductant is equal to a constant volume doseprovided by an injector of the exhaust aftertreatment system. The methodincludes pulsing, by the controller, the injector to provide theconstant volume dose of the liquid reductant based on determining thatthe amount of the liquid reductant to be injected is equal to thethreshold amount.

These and other features, together with the organization and manner ofoperation thereof, will become apparent from the following detaileddescription when taken in conjunction with the accompanying drawings,wherein like elements have like numerals throughout the several drawingsdescribed below.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 is a schematic view of an SCR system according to an exemplaryembodiment.

FIGS. 2 through 6 show cross-sectional views of the inlet section of thesystem of FIG. 1 having different injector arrangements according tovarious exemplary embodiments.

FIGS. 7 through 12 show test data for an exemplary differential DEFdosing system.

FIG. 13 is a schematic view of single reductant injector SCR systemaccording to an exemplary embodiment.

FIGS. 14A and 14B are schematic views of a two reductant injector SCRsystem according to an exemplary embodiment.

FIG. 15 is a schematic view of a two reductant injector SCR systemaccording to another exemplary embodiment.

DETAILED DESCRIPTION

Referring to the figures generally, an SCR system that utilizes constantvolume, variable timing reductant injection (e.g., a constant doseamount of DEF at variable time intervals between successive doses) totreat exhaust gases from a diesel internal combustion engine isdescribed. The SCR system periodically injects a constant volume ofreductant (such as DEF) into an exhaust system component (e.g., anexhaust pipe, a catalytic converter, etc.). The fixed volume of DEF iscommensurate with the NOx reduction requirements for a given regulatoryjurisdiction. The specific constant volume of DEF is tuned to reduce thelikelihood that DEF films or deposits will form on the exhaust systemcomponent. The interval between the constant volume doses of DEF intothe exhaust is adjusted based on the amount of NOx within the exhaustgases at a given point in time. The determined amount of NOx in theexhaust gases may be predicted, may be based on actual sensor feedback,or may be based upon a combination of both predictive information andactual sensor feedback. The interval between the constant volume dosesis calculated by integrating the required DEF amount until a thresholdamount of DEF (e.g., until one dose of DEF) is reached. The describedfixed volume, variable timing DEF injection system costs less, is easierto control, has a simpler on-board diagnostic system, is more accurate,and is at less risk for DEF deposit and film formation than traditionalfixed timing, variable volume DEF injection systems. Additionally, theuse of multiple reductant injectors can be used to spread the injectedreductant out over a larger area or be used in an alternating fashion tomitigate or prevent reductant deposits, reductant wall films, andlocalized cold spots within the aftertreatment system.

Referring to FIG. 1, a schematic view of an SCR system 100 is shownaccording to an exemplary embodiment. The SCR system 100 treats exhaustgases 102 from a diesel internal combustion engine. The SCR system 100may be part of the exhaust aftertreatment system of a vehicle, anelectrical generator, a water pump, or another diesel engine powereddevice. The exhaust gases 102 enter the SCR system through an inletsection 104 (e.g., an exhaust pipe) of the exhaust system. In somearrangements, the inlet section 104 is a decomposition reactor for theDEF. The inlet section 104 is in fluid communication with a catalystassembly 106. The catalyst assembly 106 is positioned downstream of theinlet section 104 in an exhaust gas flow direction. The catalystassembly 106 includes an SCR catalyst 108 that catalyzes the reactionbetween ammonia (provided via the DEF) and the NOx into nitrogen gas andwater. The catalyst assembly 106 also includes a slip catalyst 110positioned downstream of the SCR catalyst in an exhaust flow direction.The slip catalyst 110 catalyzes the breakdown of excess ammonia prior tothe exhaust gases 102 exiting the SCR system via an outlet section 112.The outlet section 112 may route the treated exhaust gases 102 toadditional exhaust aftertreatment components or out to the ambientenvironment.

The SCR system 100 injects doses of DEF fluid into the exhaust gases 102at the inlet section 104. Accordingly, the SCR system 100 includes aninjector 114 (or other form of insertion device), a valve 116, a pump118, and a tank 120. The injector 114, the valve 116, the pump 118, andthe tank 120 are each in fluid communication with each other. The tank120 is configured to store DEF. The DEF includes urea that is heated bythe exhaust gases 102 to form ammonia. The ammonia reacts with NOx inthe exhaust gases 102 to form nitrogen gas and water. The reactionbetween the ammonia and the NOx is catalyzed by the SCR catalyst 108.The valve 116 may be a solenoid valve. Although shown as including asingle injector 114, multiple injectors 114 may be included in the SCRsystem 100. In such an arrangement, the multiple injectors 114 may becontrolled by a single valve 116 or by multiple valves 116, wherein eachof the multiple valves 116 is associated with a single injector 114. Theinlet section 104 can be sized and shaped to account for known spraypatterns of the various injector 114 arrangements and for the specificfixed volume of DEF injected by the injectors 114 (or otherwiseinserted) for a given application. Alternative injector arrangements aredescribed below with respect to FIGS. 2-6.

The operation of the SCR system 100 is controlled by a controller 122.In some arrangements, the controller 122 is an open-loop controller. Incertain embodiments, the controller 122 includes one or more modulesstructured to functionally execute the operations of the controller 122.The description herein including modules emphasizes the structuralindependence of the aspects of the controller 122, and illustrates onegrouping of operations and responsibilities of the controller 122. Othergroupings that execute similar overall operations are understood withinthe scope of the present application. Modules may be implemented inhardware and/or as computer instructions on a non-transient computerreadable storage medium, and modules may be distributed across varioushardware or computer based components.

The controller 122 receives feedback from at least one sensor 124 via asensor feedback module. In the embodiment shown in FIG. 1, thecontroller 122 receives feedback from two sensors 124. A first of thesensors 124 is positioned upstream of the injector 114. A second of thesensors 124 is positioned downstream of the slip catalyst. Althoughshown as including two sensors 124, any number of sensors may be usedwith the SCR system 100. The sensors 124 may include any of NOx sensors,ammonia sensors, temperature sensors, pressure sensors, mass air flowsensors, or other sensors. The controller 122 may also receive data fromthe internal combustion engine control unit (“ECU”) via an ECU feedbackmodule. Such data may include the engine speed, fuel characteristics,intake air characteristics, and the like. In some arrangements, thecontroller 122 also functions as the engine control unit. The controller122 operates the pump 118 and the valve 116 to periodically inject (orotherwise insert) constant volume doses of DEF from the tank 120 intothe inlet section 104 via the injector 114 through an injector controlmodule. The controller 122 instructs the periodic constant volume dosesof DEF at variable time intervals between successive doses. Each dose orinjection may be referred to as a pulse. Because each pulse of DEF intothe inlet section 104 is a constant or fixed volume of DEF, thefrequency of the pulses of DEF into the inlet section 104 controls thetotal amount of DEF injected. As described in further detail below, thetime intervals between successive doses are calculated by integratingthe amount of DEF required by the system 100 over time until a thresholdamount of DEF is reached, and then instructing a dose of DEF when thethreshold amount of DEF is reached. The time intervals may be determinedby a timing module of the controller 122 or the injector control moduleof the controller 122. In some arrangements, the threshold amount of DEFis the fixed volume of DEF delivered with each dose.

Referring to FIG. 2, a cross-sectional view of the inlet section 104 isshown with an exemplary injector arrangement 200. The injectorarrangement 200 of FIG. 2 includes four separate injectors 114. Althoughfour injectors 114 are shown, any number of injectors 114 may bearranged along the inlet section 104 (or another section) in a similarconfiguration. Each of the injectors 114 is configured to deliver afixed amount of DEF into the inlet section 104 during each dose. Asingle valve 116 is in fluid communication with each of the fourinjectors 114 and provides DEF from the tank 120 to each injector 114via the pump 118. When the valve 116 is opened and closed by thecontroller, a dose of DEF flows through each of the injectors.

Referring to FIG. 3, a cross-sectional view of the inlet section 104 isshown with another exemplary injector arrangement 300. The injectorarrangement 300 is similar to the injector arrangement 200 of FIG. 2.The primary difference between the injector arrangement 300 and theinjector arrangement 200 is that each injector 113 of arrangement 300has a dedicated valve 116. Accordingly, each injector 114 isindividually actuable by the controller 122. Accordingly, in certaincircumstances, the controller 122 can inject DEF into the inlet section104 through less than all four of the injectors 114 (e.g., through one,two, or three of the injectors 114). Further, in the embodiment of FIG.3 (as well as other embodiments described herein), each injector 114 maybe controlled to inject a different constant dose of DEF than anotherinjector 114. For example, a first injector 114 (e.g., the far leftinjector of FIG. 3) can be configured to deliver 0.30 mL of DEF witheach dose, while a second injector 114 (e.g., the far right injector ofFIG. 3) can be configured to deliver 0.15 mL of DEF with each dose.

Referring to FIG. 4, a cross-sectional view of the inlet section 104 isshown with another exemplary injector arrangement 400. The injectorarrangement 400 includes an injection tube 402 having a plurality ofopenings 404, 406, 408, and 410. Although the injection tube 402 isshown as having four openings, any number of openings can be present.The injection tube 402 is in fluid communication with the valve 116 suchthat the valve 116 provides the injection tube 402 with DEF from thetank 120 to each injector 114 via the pump 118. The provided DEF flowsthrough the injection tube 402 and into the inlet section 104 throughthe plurality of openings 404, 406, 408, and 410. Each of the pluralityof openings 404, 406, 408, and 410 has a respective opening size D1, D2,D3, and D4. In some arrangements, the plurality of openings 404, 406,408, and 410 may be circular openings. In such arrangements, the openingsizes D1, D2, D3, and D4 are diameters of the respective openings. Asshown in FIG. 4, each of the plurality of openings 404, 406, 408, and410 has a decreasing respective opening size D1, D2, D3, and D4 (asviewed from left to right in FIG. 4). Each of the plurality of openings404, 406, 408, and 410 is sized and shaped to deliver a different fixedamount of DEF for each dose of the injection tube 402. In an alternativearrangement, each of the plurality of openings 404, 406, 408, and 410are similarly sized and shaped. In still another arrangement, some ofthe openings 404, 406, 408 and 410 may be similarly sized and/or shaped,while others are not similarly sized and/or shaped, e.g., two of theopenings 404, 406 may be of one size, while the other openings 408 and410 may be of another size.

Referring to FIG. 5, a cross-sectional view of the inlet section 104 isshown with another exemplary injector arrangement 500. The injectorarrangement 500 includes an injector insert 502. The injector insert 502is generally crescent shaped. The injector insert 502 is inserted withinthe inlet section 104 and is coupled to the interior wall of the inletsection 104. The injector insert 502 includes five injector ports 504.The injector insert 502 is in fluid communication with the valve 116such that the valve 116 provides the injector insert 502 with DEF fromthe tank 120 to each injector 114 via the pump 118. The provided DEFflows into the injector insert 502 and out the injector ports 504 intothe inlet section 104. The injector ports 504 are oriented at differentangles within the inlet section 104 about the center of the inletsection 104, which provides for a more even distribution of the DEFwithin the inlet section 104. The more even distribution of the DEFwithin the inlet section 104 further reduces the risk of DEF film andbuildup formation on the components of system 100. Each of the injectorports 504 may be of uniform size and shape or may have different sizesand/or shapes. Although only one injector insert 502 is shown in theinlet section 104, multiple injector inserts 502 may be arranged inseries along the length of the inlet section 104. In such arrangement,the injector inserts 502 may be arranged at different angles within theinlet section with respect to the central axis of the inlet section 104.

Referring to FIG. 6, a cross-sectional view of the inlet section 104 isshown with yet another exemplary injector arrangement 600. The injectorarrangement 600 includes a plurality of injector inserts 602. Eachinjector insert 602 is shaped like a sector of an annulus and is coupledto the interior wall of the inlet section 104. Each injector insert 602includes an injector port 604. Each injector insert 602 is in fluidcommunication with the valve 116 such that the valve 116 provides eachinjector insert 602 with DEF from the tank 120 to each injector 114 viathe pump 118. The provided DEF flows into the injector inserts 602 andout the injector ports 604 into the inlet section 104. In an alternativearrangement, each injector insert 602 is associated with a dedicatedvalve 116 such that each injector insert 602 is independentlycontrollable by the controller 122. The injector inserts 602 areoriented at different angles within the inlet section 104 about thecenter of the inlet section 104, which provides for a more evendistribution of the DEF within the inlet section 104. The more evendistribution of the DEF within the inlet section 104 further reduces therisk of DEF film and buildup formation on the components of system 100.Each of the injector ports 604 may be of uniform size and shape or mayhave different sizes and/or shapes. Although only a single set ofinjector inserts 602 is shown in the inlet section 104, multiple sets ofinjector inserts 602 may be arranged in series along the length of theinlet section 104. In such arrangement, the injector inserts 602 may bearranged at different angles within the inlet section with respect tothe central axis of the inlet section 104.

Referring again to FIG. 1, the controller 122 controls the operation ofthe system 100. As diesel fuel is combusted by the engine and exhaustgas 102 flows through the system 100, the controller 122 determines howmuch DEF is required to be injected into the inlet section 104 based onhow much NOx is generated by the engine. The amount of NOx generated bythe engine varies based on engine operating parameters, such as enginespeed, engine load, air quality, fuel quality, and other parameters. Thecontroller 122 receives feedback from the engine (e.g., from the engineECU, from sensors coupled to the engine, etc.) and feedback from thesensors 124 to determine how much DEF is required by the system 100 as afunction of time. The controller 122 integrates the amount of DEFrequired as a function of time to determine a total amount of DEFrequired for a given time period. When the total amount of DEF requiredis approximately equal to a threshold amount of DEF (e.g., the amount ofDEF provided by the constant volume dose), the controller 122 instructsthe pump 118 and valve 116 to inject the constant dose into the inletsection 104. As the engine operation varies, the amount of time it takesto reach the threshold amount of DEF varies. Accordingly, the amount oftime between constant volume doses via the injector 114 varies. In somearrangements, the controller 122 predicts a future amount of NOxgenerated by the engine such that the controller 122 is one or two dosesof DEF ahead of the actual requirement. In such arrangements, the system100 better handles DEF deficit situations (e.g., situations in whichthere is a sudden jump of actual NOx in the exhaust gases 102 and thesystem is behind in treating the NOx with DEF) by introducing a surplusof DEF into the system. In other arrangements, the system 100 mitigatesthe risk of DEF deficit situations by including an ammonia storagecomponent that stores ammonia within the inlet section 104 or thecatalyst assembly 106. In such arrangements, the stored ammonia is usedto treat the exhaust gases 102 during periods of increased NOx content.The amount of ammonia stored can be tailored to minimize ammonia slipfrom the system 100.

The variable time interval between successive pulses of DEF assists inpreventing DEF film and deposit formation within the inlet section 104and the catalyst assembly 106. During low temperature operations, afixed time interval, variable volume DEF dosing system is susceptible tohigh DEF dose volume error (as described above). In some situations,this error results in significant amounts of excess DEF, which may notbreak down into ammonia during the low temperature operation. The excessDEF may form deposits or films on interior portions of the inlet section104 and the catalyst assembly 106, which can reduce the system'sefficiency in treating NOx. The system 100, however, has the timingflexibility to avoid excess pulses of DEF when the pulse of DEF is notneeded, which also helps to control surface temperatures of the inletsection 104 where the DEF is sprayed. Further, the constant volumepulses of DEF are more accurate than variable volume pulses. Thesefactors combine to reduce the occurrence of excess DEF within the system100, thereby reducing the risk of DEF deposits or films forming on thevarious exhaust aftertreatment components.

The system 100 is modular such that additional systems can be used withthe same exhaust aftertreatment system if a higher volume of DEF isrequired than can be delivered through a single SCR system. For example,in a high horsepower diesel engine, large amounts of diesel fuel arecombusted to generate power. Accordingly, the high horsepower dieselengine generates larger than normal amounts of NOx when compared to anormal or small sized diesel engine. Multiple SCR systems 100 may beemployed along the exhaust system of the high horsepower diesel engine.

Referring to FIGS. 7 through 12, test data for a differential DEF dosingsystem (e.g., system 100 as described above with respect to FIGS. 1through 6) is shown. FIGS. 7 through 10 highlight normal testingconditions for 1230 ms (1.23 seconds). The test data is generated bydosing the exhaust from a 2013 ISL 450 horsepower, hot FTP cycle dieselengine with a constant dosing quantity of 0.40 mL at variable timesbased on the amount of NOx in the exhaust stream. In a variablequantity, fixed time DEF dosing system that operates at 1 Hz (e.g., 1000doses of DEF per second), 1230 doses would be required at varying doseamounts. In the above-described constant quantity, variable time DEFdosing system (e.g., system 100), only 322 doses are required at thefixed quantity. As shown in FIG. 9, the number of doses per time periodvaries throughout the duration of the 1230 ms of operation. Groupings ofhigh numbers of doses during short time periods (e.g., as shown fromapproximately 800 ms to 850 ms) represent periods where the DEF deficitis greater than the DEF pulse quantity. The areas of DEF deficit aretreated with multiple pulses of the DEF dosing system. In a correctlyprogrammed system, DEF deficit should not occur. In such a system, thecontroller (e.g., controller 122) is actuated at least one pulse aheadof the actual requirement of DEF, which results in a slight surplus ofammonia in the exhaust system that acts as a buffer for periods of highengine use. In an alternative arrangement, ammonia storage within theexhaust system can be used as buffer for periods of high engine use toeliminate DEF deficit.

FIGS. 11 and 12 highlight the above-described test data during acatch-up situation. A catch-up situation occurs where a DEF deficitexists and the controller “catches up” to the DEF deficit by initiatingmultiple back-to-back pulses of the DEF during short time periods. Asshown best in FIG. 12, during non-DEF deficit operation (e.g., from 340ms to 80 ms), the controller instructs a DEF dose when the totalquantity of required DEF hits a threshold amount (labeled “DoseThreshold” in FIG. 12). However, during rapid increases in NOxgeneration (e.g., as caused during acceleration of a vehicle), thesystem may fall behind such that the quantity of required DEF remainsabove the threshold amount for an extended period of time (e.g., from380 ms to 390 ms). In such situations, the controller instructs a rapidseries of DEF pulses to bring the DEF deficit back down below thethreshold amount.

Referring to FIGS. 13 through 15, various schematic views of reductantdeposit and film build-up situations within an exhaust aftertreatmentsystem (e.g., an SCR system) are shown. FIG. 13 shows a schematic viewof single reductant injector SCR system 1300. The system 1300 includes areductant injector 1302 configured to inject a reductant 1304, such asDEF, into an exhaust component 1306. The reductant injector 1302 isfixed with respect to the exhaust component 1306. Accordingly, thereductant injector 1302 sprays the reductant 1304 at substantially thesame spot on the exhaust component 1306. Under high temperatureoperating conditions, the reductant 1304 is heated by the exhaust gasesand the residual heat stored in the exhaust component 1306. When thereductant 1304 receives enough thermal energy, the reductant 1304 atleast partially breaks down into ammonia. However, under certain lowtemperature operating conditions (e.g., at idle engine conditions), therepeated sprayings of the reductant 1304 against the exhaust component1306 can create a cold spot on the exhaust component 1306. The cold spotinhibits the breakdown of the reductant 1304 into ammonia. Accordingly,the cold spot may cause a buildup 1308 of reductant 1304 on the innerwall of the exhaust component 1306. The buildup 1308 may be a deposit orfilm of the reductant 1304.

As shown in FIGS. 14A and 14B, the constant buildup of the deposit 1308of FIG. 13 can be mitigated through the use of multiple injectors. FIGS.14A and 14B each show a schematic view of a two reductant injector SCRsystem 1400 according to an exemplary embodiment. FIG. 14A shows thesystem 1400 at a first time period, and FIG. 14B shows the system 1400at a second time period. As shown in FIG. 14A, the system 1400 includesa first reductant injector 1402 and a second reductant injector 1404.The first and second injectors 1402 and 1404 are configured to inject areductant 1406, such as DEF, into an exhaust component 1408 of anexhaust aftertreatment system. As discussed above with respect to system1300, under certain low temperature operating conditions (e.g., at idleengine conditions), the repeated sprayings of the reductant 1406 againstthe exhaust component 1408 can create cold spots on the exhaustcomponent 1408. The cold spot inhibits the breakdown of the reductant1406 into ammonia. Accordingly, the cold spot may cause buildups 1410and 1412 of reductant 1406 on the inner wall of the exhaust component1408. The buildups 1410 and 1412 may be a deposit or film of thereductant 1406. The first buildup 1410 is associated with reductant 1406sprayed from the first injector 1402. The second buildup 1412 isassociated with reductant 1406 sprayed from the second injector 1404(e.g., as shown in FIG. 14B).

The first injector 1402 and the second injector 1404 are independentactuable (e.g., the first injector 1402 is associated with a firstdedicated valve, and the second injector 1404 is associated with asecond dedicated valve). Accordingly, reductant 1406 may be selectivelysprayed from either the first injector 1402 or the second injector 1404at different times (e.g., only one of the injectors 1402 or 1404 isspraying reductant 1406 at any given time). When reductant 1406 is beingsprayed from the first injector 1402, the first buildup 1410 may buildwhile the second buildup 1412 has time to heat and decompose (e.g., asshown in FIG. 14A). Accordingly, when the first injector 1402 isactivated and the second injector 1404 is idle, the first buildup 1410may grow under low temperature operations, and the second buildup 1412may shrink. Conversely, when reductant 1406 is being sprayed from thesecond injector 1404, the second buildup 1412 may build while the firstbuildup 1410 has time to heat and decompose (e.g., as shown in FIG.14B). Accordingly, when the first injector 1402 is idle and the secondinjector 1404 is activated, the first buildup 1410 may shrink, and thesecond buildup 1412 may grow under low temperature operations. Such anarrangement prevents large deposits and films of reductant 1406 fromremaining on the exhaust component 1408 by allowing time for any formeddeposits and films to break down without reducing the capacity of thesystem 1400.

The splitting of reductant 1406 between the first injector 1402 and thesecond injector 1404 can be controlled in various ways. A first way tocontrol when to alternate reductant 1406 injections between the firstinjector 1402 and the second injector 1404 is to alternate after eachdose. A second way of control when to alternate reductant 1406injections between the first injector 1402 and the second injector 1404is to alternate after a threshold amount of reductant has been injectedby either injector. A third way to control when to alternate reductant1406 injections between the first injector 1402 and the second injector1404 is to measure the size of the buildups 1410 and 1412 and switchbetween injectors when the associated buildup reaches a threshold size(e.g., a threshold thickness, a threshold surface area, etc.). Themeasurement of the buildups 1410 and 1412 may be accomplished with asensor or another device.

A fourth way to control when to alternate reductant 1406 injectionsbetween the first injector 1402 and the second injector 1404 is monitorthe exhaust gases for unusual changes in ammonia slip, unusual increasesin NOx downstream of the system 1400, or increased pressure restrictionof the system 1400 (caused by the increased buildup of reductant 1406)and switch between injectors when an appropriate indicator is detected.A fifth way to control when to alternate reductant 1406 injectionsbetween the first injector 1402 and the second injector 1404 is tomeasure the surface temperature of the exhaust component 1408 and toswitch between injectors when the surface temperature falls below athreshold temperature. In some arrangements, the threshold temperatureis the critical temperature required to break down the reductant 1406into ammonia.

Referring to FIG. 15, a schematic view of a two reductant injector SCRsystem 1500 is shown according to another exemplary embodiment. Thesystem 1500 includes a first reductant injector 1502 and a secondreductant injector 1504. The first and second reductant injectors 1502and 1504 are configured to inject a reductant 1506, such as DEF, into anexhaust component 1508 of an exhaust aftertreatment system. As discussedabove with respect to system 1300, under certain low temperatureoperating conditions (e.g., at idle engine conditions), the repeatedsprayings of the reductant 1506 against the exhaust component 1508 cancreate cold spots on the exhaust component 1508. The cold spot inhibitsthe breakdown of the reductant 1506 into ammonia. Accordingly, the coldspot may cause buildups 1510 and 1512 of reductant 1506 on the innerwall of the exhaust component 1508. The buildups 1510 and 1512 may be adeposit or film of the reductant 1506. The first buildup 1510 isassociated with reductant 1506 sprayed from the first reductant injector1502. The second buildup 1512 is associated with reductant 1506 sprayedfrom the second reductant injector 1504. Unlike system 1400, the firstreductant injector 1502 and the second reductant injector 1504 eachspray reductant 1506 at the same time. Since both injectors 1502 and1504 are utilized concurrently, each injector 1502 and 1504 only sprayshalf of the total dose amount. Accordingly, the entire dose of reductant1506 is spread across a larger surface area of the exhaust component1508 thereby reducing the size of any cold spots formed on the exhaustcomponent 1508. Since the cold spots are reduced, the size of thebuildups 1510 and 1512 is also minimized.

Although systems 1400 and 1500 are shown as including two injectors, anynumber of injectors greater than one may be used. The higher number ofinjectors used, the more effective the systems 1400 and 1500 are atreducing or eliminating films and buildups of the reductant.

As utilized herein, the terms “approximately,” “about,” “substantially,”and similar terms are intended to have a broad meaning in harmony withthe common and accepted usage by those of ordinary skill in the art towhich the subject matter of this disclosure pertains. It should beunderstood by those of skill in the art who review this disclosure thatthese terms are intended to allow a description of certain featuresdescribed and claimed without restricting the scope of these features tothe precise numerical ranges provided. Accordingly, these terms shouldbe interpreted as indicating that insubstantial or inconsequentialmodifications or alterations of the subject matter described and claimedare considered to be within the scope of the invention as recited in theappended claims.

It should be noted that the terms “example” and/or “exemplary” as usedherein to describe various embodiments is intended to indicate that suchembodiments are possible examples, representations, and/or illustrationsof possible embodiments (and such term is not intended to connote thatsuch embodiments are necessarily extraordinary or superlative examples).

The terms “coupled,” “connected,” and the like as used herein mean thejoining of two members directly or indirectly to one another. Suchjoining may be stationary (e.g., permanent) or moveable (e.g., removableor releasable). Such joining may be achieved with the two members or thetwo members and any additional intermediate members being integrallyformed as a single unitary body with one another or with the two membersor the two members and any additional intermediate members beingattached to one another.

References herein to the positions of elements (e.g., “top,” “bottom,”“above,” “below,” etc.) are merely used to describe the orientation ofvarious elements in the figures. It should be noted that the orientationof various elements may differ according to other exemplary embodiments,and that such variations are intended to be encompassed by the presentdisclosure.

It is important to note that the construction and arrangement of thevarious exemplary embodiments are illustrative only. Although only a fewembodiments have been described in detail in this disclosure, thoseskilled in the art who review this disclosure will readily appreciatethat many modifications are possible (e.g., variations in sizes,dimensions, structures, shapes and proportions of the various elements,values of parameters, mounting arrangements, use of materials, colors,orientations, etc.) without materially departing from the novelteachings and advantages of the subject matter described herein. Forexample, elements shown as integrally formed may be constructed ofmultiple parts or elements, the position of elements may be reversed orotherwise varied, and the nature or number of discrete elements orpositions may be altered or varied. The order or sequence of any processor method steps may be varied or re-sequenced according to alternativeembodiments. Other substitutions, modifications, changes and omissionsmay also be made in the design, operating conditions and arrangement ofthe various exemplary embodiments without departing from the scope ofthe present invention.

The description herein including modules emphasizes the structuralindependence of the aspects of the controller, and illustrates onegrouping of operations and responsibilities of the controller. Othergroupings that execute similar overall operations are understood withinthe scope of the present application. Modules may be implemented inhardware and/or as computer instructions on a non-transient computerreadable storage medium, and modules may be distributed across varioushardware or computer based components. Example and non-limiting moduleimplementation elements include sensors providing any value determinedherein, sensors providing any value that is a precursor to a valuedetermined herein, datalink and/or network hardware includingcommunication chips, oscillating crystals, communication links, cables,twisted pair wiring, coaxial wiring, shielded wiring, transmitters,receivers, and/or transceivers, logic circuits, hard-wired logiccircuits, reconfigurable logic circuits in a particular non-transientstate configured according to the module specification, any actuatorincluding at least an electrical, hydraulic, or pneumatic actuator, asolenoid, an op-amp, analog control elements (springs, filters,integrators, adders, dividers, gain elements), and/or digital controlelements.

While various embodiments of the disclosure have been shown anddescribed, it is understood that these embodiments are not limitedthereto. The embodiments may be changed, modified and further applied bythose skilled in the art. Therefore, these embodiments are not limitedto the detail shown and described previously, but also include all suchchanges and modifications.

What is claimed is:
 1. A method comprising: receiving, by a controllerof an exhaust gas aftertreatment system for an internal combustionengine, feedback from a first exhaust gas sensor of the exhaust gasaftertreatment system; determining, by the controller, an amount of aliquid reductant to be inserted into exhaust gas in an inlet section ofthe exhaust gas aftertreatment system based on the feedback from thefirst exhaust gas sensor; determining, by the controller, that theamount of the liquid reductant to be inserted is equal to a thresholdamount of liquid reductant, the threshold amount of liquid reductantequal to a constant volume dose provided by an insertion device of theexhaust gas aftertreatment system; and pulsing, by the controller, theinsertion device to provide the constant volume dose of the liquidreductant based on determining that the amount of the liquid reductantto be injected is equal to the threshold amount.
 2. The method of claim1, further comprising varying, by the controller, a time intervalbetween successive doses of the constant volume dose based on thefeedback from the first exhaust gas sensor.
 3. The method of claim 1,further comprising receiving, by the controller, feedback from an enginecontrol unit of the internal combustion engine, wherein determining theamount of the liquid reductant to be injected is based on the feedbackfrom the engine control unit.
 4. The method of claim 1, wherein theinsertion device only provides the constant volume dose every time theinsertion device is pulsed by the controller.
 5. The method of claim 1,wherein the feedback from the first exhaust gas sensor comprises atleast one of a temperature of the exhaust gas, a pressure of the exhaustgas, a mass air flow of the exhaust gas, or a NO_(x) concentration ofthe exhaust gas.
 6. The method of claim 1, wherein determining theamount of the liquid reductant to be inserted into the inlet section ofthe exhaust gas aftertreatment system comprises: determining, by thecontroller, a dosage rate based on the feedback from the first exhaustgas sensor; and integrating, by the controller, the dosage rate over atarget interval.
 7. The method of claim 6, further comprising:initiating, by the controller, a timer in response to determining thatthe amount of the liquid reductant to be inserted into the inlet sectionof the exhaust gas aftertreatment system is equal to the thresholdamount of the liquid reductant; comparing, by the controller, the timerto a timer threshold; and after pulsing the insertion device to providethe constant volume dose of the liquid reductant, pulsing, by thecontroller, the insertion device to provide a second constant volumedose of the liquid reductant in response to determining that the timeris above the timer threshold.
 8. The method of claim 7, furthercomprising resetting, by the controller, the timer in response todetermining that the amount of the liquid reductant to be inserted intothe inlet section of the exhaust gas is not above the constant volume.9. The method of claim 1, further comprising receiving, by thecontroller, feedback from a second exhaust gas sensor of the exhaust gasaftertreatment system; wherein the controller determines the amount ofthe liquid reductant based on the feedback from the first exhaust gassensor and the feedback from the second exhaust gas sensor.
 10. Themethod of claim 9, wherein the feedback from the first exhaust gassensor comprises a NO_(x) concentration of the exhaust gas and thefeedback from the second exhaust gas sensor comprises at least one of atemperature of the exhaust gas, a pressure of the exhaust gas, or a massair flow of the exhaust gas.
 11. The method of claim 1, wherein thethreshold amount is equal to the constant volume dose of the liquidreductant.